Gas for selectively etching silicon nitride and process for selectively etching silicon nitride with the gas

ABSTRACT

A dry-etching gas suitable for selective etching of silicon nitride and a process for selectively dry-etching silicon nitride with the dry-etching gas are disclosed. Silicon nitride can be dry-etched with a higher selectivity or at a higher etching rate than silicon dioxide and silicon, and a process for fabricating semi-conductor devices can be simplified and devices with a novel structure can be realized.

BACKGROUND OF THE INVENTION

This invention relates to an etching gas suitable for selectively etching silicon nitride and a process for selectively etching silicon nitride with the etching gas, and more particularly to an etching gas capable of selectively etching silicon nitride with a higher selectivity or at a higher etching rate than silicon oxide and silicon and a process for etching with the etching gas.

As is well known, dry etching of silicon or its compound is carried out with a reacting gas, for example, CF₄, CF₄ +O₂, NF₃, SF₆, CHF₃, CF₄ +H₂, etc. However, in the conventional dry etching with these reacting gases, etching rates of Si, SiO₂ and Si₃ N₄ with a reacting gas such as CF₄, CF₄ +O₂, NF₃ or SF₆ are such that the etching rate of Si is highest, and the etching rate is decreased in the order of Si₃ N₄ and SiO₂. With CHF₃ or CF₄ +H₂ as the reacting gas, the etching rates of SiO₂ and Si₃ N₄ are increased, as compared with that of Si, but the etching rate ratio of Si₃ N₄ to SiO₂ is about 2-3, and thus Si₃ N₄ cannot be selectively etched.

Thus, a reacting gas such as CF₄ +O₂ or SF₆ has been used for selective etching of Si₃ N₄, but the etching rate of Si is so high that the substrate Si is liable to be etched and thus there is a risk of considerable damages. To prevent such a risk, a SiO₂ film must be provided between the Si₃ N₄ film and the substrate Si, and furthermore the SiO₂ film must be thicker owing to a low selectivity between SiO₂ and Si₃ N₄. That is, it has been so far difficult to selectively dry-etch a Si₃ N₄ film with a higher selectivity or at a higher etching rate than Si and SiO₂, and this has been a serious trouble in forming semiconductor devices.

SUMMARY OF THE INVENTION

An object of the present invention is to solve the said problems in the prior art and provide a dry etching gas capable of selectively etching Si₃ N₄ with a higher selectivity or at a higher etching rate than Si or SiO₂ and a process for selectively etching Si₃ N₄ with the dry etching gas.

To attain this object, a gas consisting of C, H and F atom species at a ratio of F to H by atom (F/H) of not more than 2, such as CH₃ F, CH₂ F or C₂ H₃ F₃ is used in the present invention as a reacting gas for etching Si₃ N₄ with a higher selectivity.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic view showing a structure of a dry-etching apparatus in a parallel plate type for use in Examples of the present invention.

FIGS. 2 to 6 are diagrams each showing the effects of the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS EXAMPLE 1

In FIG. 1, a dry-etching apparatus used in the following Examples is shown schematically. The dry-etching apparatus of this type is an apparatus in the so-called parallel plate type.

An article 4 to be etched was placed on one of a pair of electrode plates 2 and 3 provided in parallel to each other in a vacuum chamber 1, where the electrodes were disks having a diameter of 40 cm, that is, in this example, on the electrode plate 2, and the vacuum chamber 1 was evacuated to about 10⁻⁵ Torr through a gas outlet 5. Then, CH₂ F₂ was introduced into the vacuum chamber 1 through a gas inlet 6, and the pressure in the chamber 1 was maintained at about 0.03 Torr.

Then, a high frequency power was applied to the electrode plate 2 from a high frequency power source 7 to generate a plasma between the electrode plates 2 and 3. The introduced CH₂ F₂ was decomposed and excited thereby to conduct etching of the article 4.

The frequency of the high frequency power was kept constant at 13.56 MHz and the high frequency power was changed between 200 and 500 W. The resulting etching rates of Si₃ N₄, SiO₂ and Si are shown in FIG. 2.

As is apparent from FIG. 2, the etching rate of Si₃ N₄ was considerably higher than those of SiO₂ and Si when the dry etching was carried out with CH₂ F₂ as a reacting gas. Particularly with increasing high frequency power, a difference in the etching rate became considerably large between Si₃ N₄ and SiO₂ or Si, and it was found that Si₃ N₄ could be selectively etched with a higher selectivity.

EXAMPLE 2

Etching of Si₃ N₄, SiO₂ and Si was conducted in the same dry-etching apparatus as used in Example 1, while keeping the frequency and power of high frequency power constantly at 13.56 MHz and 400 W, respectively, and changing the pressure of CH₂ F₂ gas between 0.02 and 0.05 Torr. The results are shown in FIG. 3.

As is apparent from FIG. 3, when the pressure of CH₂ F₂ exceeded about 0.02 Torr, the etching rate became rapidly higher, and the etching rate of Si₃ N₄ reached about 3.00-4.00 Å/minute above about 0.03 Torr. That is, it was found that Si₃ N₄ could be selectively etched in a high etching rate ratio of Si₃ N₄ to SiO₂ and Si of at least about 10.

EXAMPLE 3

Etching rates of Si₃ N₄, SiO₂ and Si were compared in the same dry-etching apparatus as used in Example 1 with CH₃ F as a reacting gas. The etching rates were measured by keeping the frequency of the high frequency power and the pressure of CH₃ F constant at 13.56 MHz and 0.03 Torr, respectively, while changing the high frequency power between 200 and 500 W. Results are shown in FIG. 4.

As is apparent from FIG. 4, when CH₃ F was used as the reacting gas the etching rate of Si₃ N₄ was considerably larger than those of SiO₂ and Si as in the case of using CH₂ F₂ as the reacting gas, and particularly with increasing high frequency power, the etching rate ratio of Si₃ N₄ to SiO₂ and Si became very large, and it was found that Si₃ N₄ could be selectively etched in a high etching rate ratio of at least about 10.

The dependency of the etching rate on pressure was substantially same as in the case of CH₂ F₂ shown in FIG. 3.

EXAMPLE 4

This example relates to a process for preparing CH₂ F₂, where CH₂ F₂ is prepared by gas phase reaction of dichloromethane and hydrogen fluoride in the presence of a catalyst of chromium fluoride, or a catalyst prepared by mixing and molding chromium fluoride and a carrier or a catalyst of chromium fluoride supported on a carrier. One of specific processes is given below:

300 g of commercially available CrF₃.3H₂ O was molded into pellets, 6 mm in diameter and 6 mm thick, and then gradually heated in a N₂ gas stream for drying and retained at about 400° C. for 2 hours, whereby a CrF₃ catalyst was prepared.

100 ml of the catalyst was filled in a reactor made of Hastelloy C, 20 mm in inner diameter and 1 m long. CH₂ Cl₂ and HF were evaporated in evaporators at 5.4 g/hr and 7.4 g/hr, respectively, and the resulting gases were introduced into the reactor, while keeping the temperature in the reactor at 380° C. under the atmospheric pressure. After the system was thoroughly statilized, unreacted HF and formed HCl in the gas from the reactor were trapped by an alkali to remove the acids, and remaining organic matters were recovered as a liquid condensate for 5 hours.

Composition of the recovered organic matters was analyzed by gas chromatography, and the following results were obtained.

CH₂ F₂ :11.6 g

CH₂ ClF:2.8 g

CH₂ Cl₂ :3.8 g

It was found from the results that yields on the basis of the CH₂ Cl₂ fed were as follows:

CH₂ F₂ :70%

CH₂ ClF:13%

In the foregoing Examples 1 and 2, the etching rates of Si₃ N₄, SiO₂ and Si were obtained by etching them with the thus obtained CH₂ F₂.

EXAMPLE 5

This example relates to a process for preparing CH₃ F, where CH₃ F is prepared by gas phase reaction of methyl chloride and hydrogen fluoride in the presence of an aluminum fluoride catalyst, or a catalyst prepared by mixing and molding aluminum fluoride and a carrier, or a catalyst of aluminum fluoride supported on a carrier.

One of specific processes is given below.

300 g of AlCl₃.6H₂ O was dissolved in water, and 250 g of commercially available aqueous 46% hydrogen fluoride solution was slowly added thereto to form aluminum trifluoride.

Then, the solution was kept at about 70° C. under reduced pressure of about 50 mmHg to remove the by-product hydrogen chloride, excess hydrogen fluoride and most of water by evaporation, and an aluminum trifluoride paste was obtained thereby.

Then, the paste was molded into pellets, 6 mm in diameter and 6 mm thick, and then the pellets were heated and dried in a N₂ gas stream and kept at about 400° C. for 3 hours, whereby about 100 g of aluminum fluoride catalyst was obtained.

100 ml of the catalyst was filled in a reactor made of Hastelloy C, 2 mm in inner diameter and 1 m long. CH₃ Cl and HF were evaporated at 0.845 g/hr and 2.34 g/hr, respectively, in evaporators and the resulting gases were supplied to the reactor, while keeping the temperature in the reactor at 300° C. under the atmospheric pressure. After the system was thoroughly stabilized, unreacted HF and formed HCl in the gas from the reactor were trapped by an alkali to remove the acids, and the remaining organic matters were cooled and passed through a solvent for 3 hours to recover the organic matters through absorption in the solvent.

The formed CH₃ F and supplied CH₃ Cl recovered in the solvent in the above manner were analyzed by gas chromatography, and the following result was obtained:

CH₃ F:0.358 g

CH₃ Cl:1.98 g

As other products, only some low boiling compounds which seemed to have been formed by the decomposition were found.

The foregoing results show that CH₃ F was formed in the yield of 21% on the basis of the supplied CH₃ Cl and the selectivity to CH₃ F on the basis of the reacted CH₃ Cl was about 96%.

CH₃ F used as the reacting gas in Example 3 was prepared in the manner shown in this Example.

EXAMPLE 6

Relationship between the etching rate and the gas pressure was determined when Si₃ N₄, SiO₂ and Si were etched using C₂ H₃ F₃ as reacting gas, the results are shown in FIG. 5, where the flow rate of C₂ H₃ F₃ was 10 cc/minute and the applied high frequency power was 400 W.

As is apparent from FIG. 5, when C₂ H₃ F₃ was used as a reacting gas, Si₃ N₄ could be etched with a higher selectivity or at a higher etching rate than SiO₂ and Si in the same manner as in the foregoing Examples.

EXAMPLE 7

Etching was carried out with C₂ H₅ F, C₂ H₄ F₂, C₂ H₃ F₃, C₂ H₂ F₄, C₃ H₇ F, C₃ H₆ F₂, C₂ H₅ F₃, C₃ H₄ F₄ and C₃ H₃ F₅ as reacting gas in the same manner as in the foregoing Examples, and it was found that Si₃ N₄ could be etched with a higher selectivity, and that Si₃ N₄ could be selectively etched with many gases each consisting of C, H and F atom species and having a ratio of F to H by atom of not more than 2.

On the other hand, no good results were obtained with the gases having a ratio of F to H of more than 2 such as CHF₃ or C₂ HF₅.

With increasing C number, undersirable phenomena such as an increase in deposits, etc are liable to appear.

Thus, it is most preferable to use a gas having a ratio of F to H of not more than 2, and a carbon number of not more than 3. These gases can be used alone, and Si₃ N₄ can be selectively etched even with a mixture of at least two kinds of these gases.

EXAMPLE 8

In this Example, a mixture of two kinds of gases, which satisfied the conditions as mentioned above, i.e. a gas consisting of C, H and F atom species, and having a ratio of F to H by atom of not more than 2, was used. That is, etching rates were measured by changing a mixing ratio of CF₂ to H₂ to various degrees, and results are shown in FIG. 6.

As is apparent from FIG. 6, Si₃ F₄ could be etched with a mixture of gases with a higher selectivity, so long as the mixture of gases can satisfy the conditions as mentioned above, that is, so long as the mixture of gases consists of C, H and F atom species and has a ratio of F to H by atom of not more than 2. It is needless to say that mixtures of other gases than CF₄, for example, CHF₃, etc. can be used, so long as the mixtures of gases can satisfy the condition as mentioned above.

However, it is often desirable from practical viewpoints of gas stability, uniform composition, etc. to use a gas having a composition satisfying the condition as mentioned above rather than to use a mixture of a plurality of gases to satisfy the conditions as mentioned above.

Gases each having a composition satisfying the condition as mentioned above can be used alone, but also can be used in a combination in an appropriate ratio, or a plurality of gases can be mixed to satisfy the condition as mentioned above, though practically not so preferable, as pointed out above.

At the etching, the gas pressure in the reactor is usually about 10⁻² Torr, but can be appropriately selected, depending upon the mode of etching.

It is also possible to add at least one of other gases such as N₂, O₂, H₂ or He to the etching gas.

As described above, Si₃ N₄ can be etched at a higher etching rate than SiO₂ and Si according to the present invention, and thus where there are SiO₂ or Si besides Si₃ N₄ at the same time, Si₃ N₄ can be selectively etched. For example, where a Si₃ N₄ film is formed on a substrate of SiO₂ or Si, or on a polycrystalline silicon film, only the Si₃ N₄ film can be etched without giving any substantial damage to the substrate or the polycrystalline silicon film. It is also possible to selectively etch the Si₃ N₄ film by masking the SiO₂ film or polycrystalline silicon film, and, where there are Si₃ N₄, SiO₂ and Si on a wafer at the same time, only Si₃ N₄ can be etched while leaving SiO₂ or Si as it is.

In dry-etching Si₃ N₄ according to the conventional dry etching process, it is impossible to dry-etch Si₃ N₄ with a thoroughly higher selectivity or at a higher etching rate than SiO₂ or Si, and consequently the process for fabricating semiconductor devices are restricted to various degrees, and also the structure of semiconductor devices is limited.

According to the present invention, Si₃ N₄ can be selectively etched with a higher selectivity than SiO₂ and Si, as described above, and thus the said restriction or limitation to the process for fabricating semiconductor devices or to the structure of semiconductor devices is considerably less, and selection or design freedom of the process or device structure is considerably increased. For example, it is possible to selectively remove only the exposed parts of Si₃ N₄ film by etching according to the present invention without removing the exposed parts of SiO₂ or Si, and also to etch a Si₃ N₄ film formed on a SiO₂ film, a Si substrate or a Si film without giving any serious damage to the SiO₂ film, Si substrate or Si film as an underlayer. Furthermore, it is possible to etch a silicon nitride film by masking a silicon dioxide film or a polycrystalline silicon film.

Such a selective etching of Si₃ N₄ is quite impossible to carry out according to the conventional dry-etching process using CF₄, SF₆ or CHF₃ as a reacting gas, and is useful particularly for forming semiconductor integrated circuits with a high integration density.

In the foregoing Examples, the so-called reactive sputter-etching apparatus in a parallel plate type shown in FIG. 1 was used as a dry-etching apparatus, and the present invention has the most distinguished feature in selective etching of Si₃ N₄ with a reacting gas consisting of C, H and F atom species and having a ratio of F to H by atom of not more than 2. Thus, the dry-etching apparatus for use in the present invention is not restricted to the said apparatus in a parallel plate type, and Si₃ N₄ can be selectively etched in various kinds of well known dry-etching apparatus such as the so-called microwave plasma etching apparatus that generates plasma by microwave excitation, or a planar magnetron-type plasma etching apparatus. Better results can be obtained in a dry-etching apparatus in a parallel plate type when a reacting gas pressure is in a range of 0.01-0.1 Torr. In a dry-etching apparatus of other type, an appropriate reacting gas pressure is selected. 

What is claimed is:
 1. A gas for selectively etching silicon nitride, which comprises a composition consisting of C, H and F atom species and having a ratio of F to H by atom of not more than
 2. 2. A gas according to claim 1, wherein the gas has a carbon number of not more than
 3. 3. A gas according to claim 1 or 2, wherein the gas is at least one member selected from the group consisting of CH₂ F₂, CH₃ F, C₂ H₅ F, C₂ H₄ F₂, C₂ H₃ F₃, C₂ H₂ F₄, C₃ H₇ F, C₃ H₆ F₂, C₃ H₅ F₃, C₃ H₄ F₄ and C₃ H₃ F₅.
 4. A process for etching an article by contact of the article with a plasma of a reacting gas, which comprises selectively etching silicon nitride as the article with a gas consisting of C, H and F atom species and having a ratio of F to H by atom of not more than 2 as the reacting gas.
 5. A process according to claim 4, wherein the reacting gas has a carbon number of not more than
 3. 6. A process according to claim 4 or 5, wherein the reacting gas is at least one member selected from the group consisting of CH₂ F₂, CH₃ F, C₂ H₅ F, C₂ H₄ F₂, C₂ H₃ F₃, C₂ H₂ F₄, C₃ H₇ F, C₃ H₆ F₂, C₃ H₅ F₃, C₃ H₄ F₄ and C₃ H₃ F₅.
 7. A process according to claim 4, wherein the etching is carried out in a reactive sputter etching apparatus in a parallel plate type.
 8. A process according to claim 7, wherein the reacting gas has a pressure of 0.01-0.1 Torr.
 9. A process according to claim 4, wherein at least one of silicon dioxide film and polycrystalline silicon film, and a film of the silicon nitride are exposed to surface.
 10. A process according to claim 9, where the film of the silicon nitride is etched by masking the silicon dioxide film or the polycrystalline silicon film or both.
 11. A process according to claim 4, wherein the film of the silicon nitride is formed on a silicon substrate, the polycrystalline silicon film or the silicon dioxide film.
 12. A process according to claim 4, wherein the reacting gas is mixed with at least one member selected from the group consisting of N₂, O₂, H₂ and He.
 13. A process according to claim 4, wherein the reacting gas is a mixture of at least one of CF₄ and CHF₃, and H₂. 